Liquid-liquid equilibria of butyric acid for solvents containing a phosphonium ionic liquid

被引:62
作者
Martak, Jan [1 ]
Schlosser, Stefan [1 ]
机构
[1] Slovak Tech Univ Bratislava, Fac Chem & Food Technol, Inst Chem & Environm Engn, Bratislava 81237, Slovakia
关键词
extraction; L/L equilibria; butyric acid; phosphonium ionic liquid; modelling;
D O I
10.2478/s11696-007-0077-5
中图分类号
O6 [化学];
学科分类号
0703 ;
摘要
L/L equilibrium data of butyric acid (BA) in aqueous solutions contacted with the solvents containing ionic liquid (IL), trihexyl-(tetradecyl)phosphonium bis 2,4,4-trimethylpentylphosphinate (Cyphos IL-104), and a related model are presented. IL-104 and its solutions in dodecane were found to be effective solvents of BA. The values of the distribution coefficients of BA were higher than those for solvents with the widely used extractant trioctylamine, especially at low acid concentrations and were also several-fold higher than those of lactic acid (LA). IL extracted BA only in its undissociated form (BAH) at pH well below pK (a) of the acid. The loading of IL was independent of IL concentration and it achieved a value higher than four at saturation. Complexes with 1-5 molecules of BA per one IL molecule were supposed in the mass action model in which the reactive formation of complexes (BAH) (p) (IL)(H(2)O)(2) was supposed. Up to 10 % of the total extracted BA was extracted physically by dodecane as a monomer and dimer, in the solvent. The water content in the organic phase steeply decreased with the BA concentration, which was caused by splitting water-IL reverse micelles due to the formation of the BAH/IL complexes. (c) 2008 Institute of Chemistry, Slovak Academy of Sciences.
引用
收藏
页码:42 / 50
页数:9
相关论文
共 38 条
[1]  
Bekou E, 2003, ACS SYM SER, V856, P544
[2]   Distribution of butyric acid between water and several solvents [J].
Bilgin, Mehmet ;
Kirbaslar, S. Ismail ;
Ozcan, Onder ;
Dramur, Umur .
JOURNAL OF CHEMICAL AND ENGINEERING DATA, 2006, 51 (05) :1546-1550
[3]   Industrial preparation of phosphonium ionic liquids [J].
Bradaric, CJ ;
Downard, A ;
Kennedy, C ;
Robertson, AJ ;
Zhou, YH .
GREEN CHEMISTRY, 2003, 5 (02) :143-152
[4]  
Cardoso MM, 1999, J CHEM TECHNOL BIOT, V74, P801, DOI 10.1002/(SICI)1097-4660(199908)74:8<801::AID-JCTB107>3.0.CO
[5]  
2-Y
[6]  
Cull SG, 2000, BIOTECHNOL BIOENG, V69, P227
[7]   EXTRACTION EQUILIBRIA OF ORGANIC-ACIDS WITH TRI-N-OCTYLPHOSPHINEOXIDE [J].
HANO, T ;
MATSUMOTO, M ;
OHTAKE, T ;
SASAKI, K ;
HORI, F ;
KAWANO, Y .
JOURNAL OF CHEMICAL ENGINEERING OF JAPAN, 1990, 23 (06) :734-738
[8]   EXTRACTIVE FERMENTATION SYSTEMS FOR ORGANIC-ACIDS PRODUCTION [J].
HATZINIKOLAOU, DG ;
WANG, HY .
CANADIAN JOURNAL OF CHEMICAL ENGINEERING, 1992, 70 (03) :543-552
[9]   Room temperature ionic liquids as novel media for 'clean' liquid-liquid extraction [J].
Huddleston, JG ;
Willauer, HD ;
Swatloski, RP ;
Visser, AE ;
Rogers, RD .
CHEMICAL COMMUNICATIONS, 1998, (16) :1765-1766
[10]   Design and simulation of two phase hollow fiber contactors for simultaneous membrane based solvent extraction and stripping of organic acids and bases [J].
Kertész, R ;
Schlosser, S .
SEPARATION AND PURIFICATION TECHNOLOGY, 2005, 41 (03) :275-287